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Co-generation of synthesis gas and C_(2+) hydrocarbons from methane and carbon dioxide in a hybrid catalytic-plasma reactor: A review

机译:混合等离子体催化反应器中甲烷和二氧化碳的联产合成气和C_(2+)碳氢化合物:综述

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摘要

The topics on conversion and utilization of methane and carbon dioxide are important issues in tackling the global warming effects from the two greenhouse gases. Several technologies including catalytic and plasma have been proposed to improve the process involving conversion and utilization of methane and carbon dioxide. In this paper, an overview of the basic principles, and the effects of CH_4/CO_2 feed ratio, total feed flow rate, discharge power, catalyst, applied voltage, wall temperature, and system pressure in dielectric-barrier discharge (DBD) plasma reactor are addressed. The discharge power, discharge gap, applied voltage and CH_4/CO_2 ratio in the feed showed the most significant effects on the reactor performance. Co-feeding carbon dioxide with the methane feed stream reduced coking and increased methane conversion. The H_2/CO ratio in the products was significantly affected by CH_4/CO_2 ratio. The synergism of the catalyst placed in the discharge gap and the plasma affected the products distribution significantly. Methane and carbon dioxide conversions were influenced significantly by discharge power and applied voltage. The drawbacks of DBD plasma application in the CH_4-CO_2 conversion should be taken into consideration before a new plausible reactor system can be implemented.
机译:甲烷和二氧化碳的转化和利用是解决两种温室气体对全球变暖的重要问题。已经提出了包括催化和等离子体的几种技术来改进涉及甲烷和二氧化碳的转化和利用的过程。本文概述了介质阻挡放电(DBD)等离子体反应器中CH_4 / CO_2进料比,总进料流速,放电功率,催化剂,施加电压,壁温和系统压力的基本原理及其影响已解决。进料中的放电功率,放电间隙,施加的电压和CH_4 / CO_2比对反应器性能显示出最显着的影响。将二氧化碳与甲烷进料流共同进料可减少焦化并提高甲烷转化率。产品中的H_2 / CO比值受到CH_4 / CO_2比值的显着影响。放置在放电间隙中的催化剂与等离子体的协同作用显着影响了产物的分布。甲烷和二氧化碳的转化率受放电功率和施加电压的影响很大。在可以实施新的合理的反应器系统之前,应考虑将DBD等离子体应用于CH_4-CO_2转化的缺点。

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